FSD100MbP?h㈵>dkS*$@@@dfffffr@м@jl[Restoring flowsheet from file Loaded controller.fsd x temperaturepressure compositionflow e@0m@E@`Y@@FLast runP2 `m@Z}@.@h@@FProfilesP  a@he@G@Q@@FLast runP C1_C2 (EOS)ڐ@'t+@-<-ethane production:0yE>MbP?MbP?MbP?%c:\werk\CO\COCO\bin\data\ChemSep1.pcdaEthyleneCH2CH2C2H474-85-1C=C pq@:SA?I ?p-e@Z@Z@`;_@ <@%?E?F=L@s?E,A A?QA AIA 8@ض@,=@ A 8 8 8IR@Z@@@)?¥q@@? 8 Y@q@i@O@ |[>@Z@q@etA_v?:`I@@dZ@q@j@3ϲ@L`;Q@@Nuu?$@Y@d@q@`Y\?zX@@3?p@@@ /&@N?bI@p@@?N_v78R@^@p@h`D! \r@ $̿@ٶ@`fY@@p@e}>߄?)xv@`f 8-e@@@fnȿ"[&ӿQl@>Y@q@)>_? y@ 8@e@ \w@fkg…m@@Ou?Z@@3q@"@&AR#? BUB@>I@@@d 8 8 8 8 8 8 84@@3y@`! 8 8-e@@3o@ ڊe@R ? 8 8`fY@@p@ N@aC@֡O.삿?5^ID>@`?@ ?@ ?]K?QJ@`d;? 8 8F??<̐?`Ɔ??D@%?`%pQ@`.h@`?@?PHydrogenH2H2 1333-74-0[H][H]JQ@@4A k??c4@`f+@`f+@4@ @@?˿b=@ y? A@@ 8Ӭ 8 8 8 8 8,@@ ?Q@@s? 8+@@ @@i*@-bXh?4?@(*@Q@@ej7AE @ @r`f+@ \O@@jb@+s`mjt=WA<`f+@@3s7@dW@`fQc@ ?+@@@%@`@ 4't?g@o@p@? $J@ j>ி`0@z@hC@tSX@ӫ@=i@+@@@e >0?s `@ 8`f+@@@fտg3`q8 S?.,+@?@ e??*@N? 8$@@fyj@? ]9>cD`f+@@ @@@I"@jH`> 8Y@@@ 8 8 8 8 8 8 8n2@Q(a@ H3? 8 8 4@#=@ jM#^SJ9 8 8+@@@ MSt?@HztbX9@@U0???@v? 8 8HͿ`r?_?@I?@Px?@z@@?B?@f(>@?@?^EthaneCH3CH3C2H674-84-0CCs@ЕRA?"?g@ V@ V@z?>@?`X?=8@`?EAp~ AEA 8@I`M9@ 8 8 8`f&7@`fV@ ??@s@ G? 8p-V@`s@iAM@@3ܥ`>@`fV@`s@efvA`ff?`[1@`QxV@Gs@j`m@@3IV@@Oۀ? \/@@3S@d`@`f?@))?p-V@ r@4@^E'@@K3?}b@p@(?@3N4`#@"[*\@@h/Xz@`?@`fV@r@e>`?g@ 8`fV@@@f鲿~[#@ё@k@gy¾`fV@r@ ? ?`f@덋 8g@@@fG!>@* `9Me?QxV@s@@@lgBO?B >I@@@d 8 8 8 8 8 8 8E4@@3@  8 8@3f@q@ @;j o? 8 8`fV@r@ NbX9/@̆(|x#?*Pz}>@?"?"?@>?+@ B? 8 8`0*??@t]??<,?zF@?)@)i@ ? B?MNitrogenN2N2 7727-37-9N#NJ̌_@IA ?~?`fVS@`O@`O@t@<@`֡??=@-?d6A``A%A 8 \B@ۮ 8 8 8`f4@@3O@@z@@r?G_@`;? 8@3O@࣐_@iBD@|@??@ gN@࣐_@e"zAY5@ 33@+@3O@࣐_@jHnA]@`-'``?@%5@`f @ 8@3O@Ȟ@f˿$@ u7?&eN@_@`?6?@^?@3@@^r@ 8I@@@f@d5X@Ֆ3?`7@3O@̌_@@@`]\AC? P`>4AI@@@d 8 8 8 8 8 8 8zt4@V@@ 8 8S@ ;\@ \@Cqd? 8 8@3O@@_@ QkwjA@R빍bX9@?rh?rh?= ?`@`? 8 8ZT?`?@"???2@`֡?lD @֜W@0?`?bubblePointTemperaturebubblePointTemperaturedensitydensitydensity/volume (pure)density/volume (pure)dewPointTemperaturedewPointTemperature enthalpyenthalpy enthalpyF enthalpyFentropyentropy!entropyFentropyFfugacityfugacityfugacityCoefficientfugacityCoefficient heatCapacityheatCapacityCpKK logFugacityCoefficientlogFugacityCoefficientsurfaceTensionsurfaceTensionsurfaceTension (pure)surfaceTension (pure)thermalConductivitythermalConductivity04thermalConductivity (pure)thermalConductivity (pure))1 viscosity viscosity& viscosity (pure)viscosity (pure)" volumevolumeVapor Vapor phaseLiquid Liquid phase   T8m4?'Hydrogen/Ethylene T=123.15-248.15K p229imported from PR.IPDtF_?)Ethylene/C2 T=200-255K P=2.2-26.7bar p503imported from PR.IPD'?Nitrogen/Ethylene p298imported from PR.IPD8m4?'Hydrogen/Ethylene T=123.15-248.15K p229imported from PR.IPDݓZ!Hydrogen/C2 T=149.61-189.57K p233imported from PR.IPD߾3? Hydrogen/Nitrogen T=90-113K p210imported from PR.IPDtF_?)Ethylene/C2 T=200-255K P=2.2-26.7bar p503imported from PR.IPDݓZ!Hydrogen/C2 T=149.61-189.57K p233imported from PR.IPD"u?Nitrogen/C2 T=200-290K p300imported from PR.IPD'?Nitrogen/Ethylene p298imported from PR.IPD߾3? Hydrogen/Nitrogen T=90-113K p210imported from PR.IPD"u?Nitrogen/C2 T=200-290K p300imported from PR.IPD  aCH2CH3ͪ?A`"? rh.@CH2M O?HzG?Zd;O ,@aCH2CH3ͪ?A`"? rh.@CH2M O?HzG?Zd;O ,@ V瞯<ethane productionethane productionbKrx-WSethane production0c:\werk\CO\COCO\bin\data\DefaultComponentLib.pcdEthane74-84-0EthaneC2H6>@Ethylene74-85-1EthyleneC2H4 <@Hydrogen 1333-74-0HydrogenH2 @ Ethane prodVapor$4.16667e-006*C(Ethylene)*C(Hydrogen)-136330?؀My>Pethane production74-84-0Ethane>@g@C2H6ethane productionEthane74-85-1Ethylene <@p-e@C2H4ethane productionEthylene 1333-74-0Hydrogen @c4@H2ethane productionHydrogen 7727-37-9Nitrogen<@`fVS@N2ethane productionNitrogen ????????????thermalConductivity.Dmoles?? / molenthalpyF.DmolFraction??viscosity.Dtemperature???? thermalConductivity.Dtemperature??thermalConductivity.Dpressure??enthalpyF.Dpressure??heatCapacity.DmolFraction??entropyF.Dmoles??enthalpy.Dmoles??density.Dpressure?@?@#logFugacityCoefficient.DmolFractionentropy.Dtemperature??viscosity.Dmoles???? / mol volume.Dmoles@@@@ enthalpyF??enthalpy??fugacity.Dtemperature??volume.Dpressure@@@@surfaceTension.DmolFraction??fugacityCoefficient.Dmoles / molenthalpy.DmolFraction??logFugacityCoefficiententhalpy.Dpressure?? fugacityCoefficient.DmolFractionfugacity.Dpressuredensity?@?@volume.DmolFraction@@@@enthalpyF.Dtemperature??surfaceTension.Dtemperature??thermalConductivity??entropyF.DmolFraction??density.DmolFraction?@?@surfaceTension??heatCapacity.Dtemperature??#logFugacityCoefficient.DtemperaturefugacityCoefficient.Dpressureviscosity.DmolFraction????entropy.Dpressure??enthalpy.Dtemperature??surfaceTension.Dmoles?? / mol thermalConductivity.DmolFraction??density.Dmoles?@?@ / mollogFugacityCoefficient.Dmoles / molsurfaceTension.Dpressure??enthalpyF.Dmoles??entropyF.Dtemperature??entropy.DmolFraction??entropy??volume@@@@entropyF??heatCapacity.Dpressure??fugacityCoefficientviscosity.Dpressure?? logFugacityCoefficient.DpressureentropyF.Dpressure?? fugacityCoefficient.Dtemperatureentropy.Dmoles?? heatCapacity?? viscosity????volume.Dtemperature@@@@density.Dtemperature?@?@fugacity.Dmoles?? / molheatCapacity.Dmoles??@ &{776B42B7-D0E5-4C4B-87E8-E1C4AAD38C32} Pressure drop?? Temperature?? Heat duty??Reactor volume@@@@ Catalyst mass??Catalyst volume@@@@Catalyst density@?@?TotalMassBalancePropertiesFraction?? TotalFlowMass??&{FCC17C95-0B2E-4946-B873-A35B10C4B6E1} Pressure drop?? Temperature?? Heat duty??&{603DF4B9-4F88-475D-A458-85F56125DA70} Pressure drop?? Temperature?? Heat duty??ReactionPackagePropertiesrate-homogeneous?@?@&{43312205-B251-4EEB-B585-4D82BB019C56}%Length??Diameter?? Roughness?? Temperature?? Heat duty??Catalyst loading@?@?Catalyst particle diameter??Wall heat transfer coefficient??Ambient Temperature??Heating/cooling tube diameter??Tube heat transfer coefficient?? Heating/Cooling tube temperature??Position?? Ethane flow?? Ethylene flow?? Hydrogen flow??Pressure?? Total flow??Density?@?@ Viscosity??Superficial velocity??Rate Ethane prod?@?@ EnthalpyF??Ethane flow profile??Ethylene flow profile??Hydrogen flow profile??Temperature profile??Pressure profile??Total flow profile??Density profile?@?@Viscosity profile????Superficial velocity profile??Ethane prod rate profile?@?@EnthalpyF profile??Enthalpy profile?? Tolerance??Catalyst porosity??&{EF130956-4BC7-49EB-8B04-65965125EA19} streamParams#Component mole flow(Ethane)@kg1@s-1??$Component mole flow(Ethane)@s-1@mol1??&Component mole flow(Ethylene)@s-1@mol1?? Length@m1??&{708D633D-65E6-4C80-9C7F-55206BD6F1C4}COFE_ControllerEbubblePointTemperaturedensitydensity.Dmolesdensity.DmolFractiondensity.Dpressuredensity.DtemperaturedewPointTemperatureenthalpyenthalpy.Dmolesenthalpy.DmolFractionenthalpy.Dpressureenthalpy.Dtemperatureentropyentropy.Dmolesentropy.DmolFractionentropy.Dpressureentropy.Dtemperaturefugacityfugacity.Dmolesfugacity.DmolFractionfugacity.Dpressurefugacity.DtemperaturefugacityCoefficientfugacityCoefficient.Dmoles fugacityCoefficient.DmolFractionfugacityCoefficient.Dpressure fugacityCoefficient.Dtemperature heatCapacityheatCapacity.DmolesheatCapacity.DmolFractionheatCapacity.DpressureheatCapacity.DtemperaturelogFugacityCoefficientlogFugacityCoefficient.Dmoles#logFugacityCoefficient.DmolFraction logFugacityCoefficient.Dpressure#logFugacityCoefficient.DtemperaturesurfaceTensionsurfaceTension.DmolessurfaceTension.DmolFractionsurfaceTension.DpressuresurfaceTension.DtemperaturethermalConductivitythermalConductivity.Dmoles thermalConductivity.DmolFractionthermalConductivity.Dpressure thermalConductivity.Dtemperature viscosityviscosity.Dmolesviscosity.DmolFractionviscosity.Dpressureviscosity.Dtemperaturevolume volume.Dmolesvolume.DmolFractionvolume.Dpressurevolume.DtemperaturebubblePointPressuredewPointPressure enthalpyFenthalpyF.DmolesenthalpyF.DmolFractionenthalpyF.DpressureenthalpyF.DtemperatureentropyFentropyF.DmolesentropyF.DmolFractionentropyF.DpressureentropyF.DtemperatureVaporethane productionVaporLiquidethane productionLiquid VaporLiquiddefaultdefault material templateethane productionr feed default`6Ar@?h-C6?|=?Report Intervals$Number of slices for output profilesd Packed bedReactor has catalyst packingCatalyst loading Catalyst mass per reactor volume@?חACatalyst porosity'Relative void space of catalyst packingffffff?ffffff??Catalyst particle diameter,Particle diameter for catalyst pressure drop?MbP?MbP?|=?Wall heat transfer coefficient?Heat transfer coefficient for heat transfer to the reactor wall?@Y@ _BAmbient Temperature9Ambient temperature for heat transfer to the reactor wall?fffffr@fffffr@ _BNumber of heating/cooling tubesNumber of heating/cooling tubes'Heating/cooling tube diameter<Tube diameter for heat transfer to the heating/cooling tubes? F%u? F%u?|= _BTube heat transfer coefficientHHeat transfer coefficient for heat transfer to the heating/cooling tubes?@ _B Heating/Cooling tube temperature:Temperature for heat transfer to the heating/cooling tubes?fffffx@fffffx@ _B Ethane prod PositionPosition along the reactor?e,+?,+?!ԏ?,+?F1B[?!ԏ?/xR*?,+?q?F1B[??!ԏ?du&qpC?/xR*?3?,+?o^mW?q??F1B[?#ڽ,??+Y?!ԏ?B}r?du&qpC?Ra?/xR*? !C?3? r$AZ?,+?M?o^mW?;紟?q?gnB??(?F1B[?,E?#ڽ,?N.6N??oo&f?+Y?L8?!ԏ?))e ?B}r??du&qpC?z?Ra?#{}?/xR*?7N? !C?Y{u5 ?3?zX? r$AZ?5ǜ?,+?pL?M?~e?o^mW?n7?;紟?!j_c?q?BP?gnB?dd@??Ae1z|?(?S&@F1B[@}[ @,E@u쯁H@#ڽ,@[`@N.6N@Xr@@'8S2@oo&f@c@+Y@HV۰@L8@كS_l@!ԏ@i @))e @`SD=@B}r@Ethane flow profile%Ethane flow profile along the reactor?eِ|܂Q9?*FVH?>LQ?W'KK&W? O\?r"`?Wc?WHe?vg?eMe>i?UJB}?PH}?ꨳ0<~?s|~?]&c}~?T!~?;/?S;f?pD?B?;X?*2?d/?\lF?[?qDhp?5͋? 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IW7?:7?~Ӛ7?*~d7?=![7?}7?P7?7an=7?M7? ߙ7?2Y 7?X 7?ƬAⶪ7?@U@7?Ys7?X37?Ethane prod rate profile*Ethane prod rate profile along the reactor@?e!fT?R@?VD ?Ɨyϼ?=?s|V-?+&!*??|ZB?P%r?˜ި?kYk?_A+?}Ӝ?7p?!&H?{)6u ?"Gٹ?~%R?s Ş?m?0lĕ?.k?؟?\vZ߲??uc ?[E?'xㆰ?]?M)J?!Č?x@ʫ?M?紹V?[ z?Am{?%e?%v?vnŤ?W\s?z\-?Qo?8S[?rZ{?a?vk?px?f67u? `YZ?qK?\˃I?S?:kh?U6?>ٱ?r?vL/) ?ğe?ԑMg?D?gcb?tŒ?qD(/? 鞑?.֓?k,珐? .B?,?RG#qAѮs@rPWr s(2bs s՗Wt/oft}tQ?ui2KPu𲷘u^yuo0 "vIJcvVr\v QүZv1F]\w[tSww4w-w*(wp#'&xSVx$Ѕxˣx71 x99j y(od4yZBΡ,]y+qxyzvyV>y5yxzCH8za$Zz"Xzz<Tz:$3za,Jzz[Az1{Jb}*{B@QROE{Van_{esx{s^8{З*Qԩ{d$`{jlf{K͇{Last run&+++ specifications +++ Using enthalpy and heat of reaction in enthalpy calculations Length: 2.55570125945363 m Diameter: 0.3 m Cross section area: 0.0706858 m Total reactor volume: 0.180652 m Number of heating/cooling tubes: 0 Roughness: 0 m Heat duty: 0 W/m Wall heat transfer coefficient: 100 W/m/K Wall perimeter: 0.942478 m Ambient Temperature: 298.15 K Flow direction: Horizontal Reaction phase: Vapor Tolerance: 0.00001 Report Intervals: 100 kinetic reaction "Ethane prod": homogeneous Compound equations: 3 Inert compounds: 1 Number of equations: 6 +++ solution +++ Solution obtained using 252 function evaluations +++ Heat Transfer results +++ Minimum temperature: 298.814639981 K Maximum temperature: 318.554037573 K Heat duty reactor wall: -1231.78607346 W ProfilesIPosition Ethane flow Ethylene flow Hydrogen flow Temperature Pressure Total flow Density Viscosity Superficial velocity r[Ethane prod] Enthalpy m mol/s mol/s mol/s K Pa mol/s mol/m Pa s m/s mol/s/m J/mol 0 0 0.01 0.01 300 1466560 0.025 600.01188812 1.24987593369e-005 0.000589451073007 0.240000330563 -111.194888556 0.0255570125945 0.000386328171304 0.0096136718287 0.0096136718287 318.160466906 1466560 0.0246136718287 563.860810886 1.3104995761e-005 0.000617549967894 0.202089917498 540.677899367 0.0511140251891 0.000742763409653 0.00925723659035 0.00925723659035 318.252062145 1466560 0.0242572365903 564.093396075 1.30877912722e-005 0.000608356171035 0.193088563403 543.022391054 0.0766710377836 0.00108463701322 0.00891536298678 0.00891536298678 317.500404761 1466560 0.0239153629868 565.931657874 1.30420166726e-005 0.000597833981735 0.185449537632 514.112587648 0.102228050378 0.00141293862236 0.00858706137764 0.00858706137764 316.735645433 1466560 0.0235870613776 567.811850282 1.29960376805e-005 0.000587674699938 0.178042321408 484.269845931 0.127785062973 0.00172802623261 0.00827197376739 0.00827197376739 315.982040984 1466560 0.0232719737674 569.687087647 1.29507162725e-005 0.000577915645338 0.170842807036 454.407194376 0.153342075567 0.00203031699135 0.00796968300865 0.00796968300865 315.241155253 1466560 0.0229696830086 571.553414563 1.29061328274e-005 0.000568546234169 0.163853989509 424.604732589 0.178899088162 0.00232015346657 0.00767984653343 0.00767984653343 314.531707653 1466560 0.0226798465334 573.372790033 1.28629573811e-005 0.000559590897407 0.15706140909 395.596780814 0.204456100756 0.00259785603785 0.00740214396215 0.00740214396215 313.858213886 1466560 0.0224021439622 575.134179412 1.28213732565e-005 0.000551046204072 0.150467914987 367.592734192 0.230013113351 0.00286392329807 0.00713607670193 0.00713607670193 313.187855456 1466560 0.0221360767019 576.901368004 1.27802698168e-005 0.000542833562232 0.144108532938 339.369267913 0.255570125945 0.00311863123572 0.00688136876428 0.00688136876428 312.541666926 1466560 0.0218813687643 578.631050338 1.27403932251e-005 0.000534983465307 0.137966036143 311.757671753 0.28112713854 0.00336247726471 0.00663752273529 0.00663752273529 311.861326107 1466560 0.0216375227353 580.440501391 1.26997515726e-005 0.000527372449163 0.132092931005 282.520606737 0.306684151134 0.00359590170717 0.00640409829283 0.00640409829283 311.328529002 1466560 0.0214040982928 581.958336633 1.2664582885e-005 0.000520322554741 0.126320048707 258.751649635 0.332241163729 0.00381911127252 0.00618088872748 0.00618088872748 310.750366793 1466560 0.0211808887275 583.575511901 1.26282958133e-005 0.000513469590424 0.120829559124 232.980954399 0.357798176324 0.0040325884979 0.0059674115021 0.0059674115021 310.204299038 1466560 0.0209674115021 585.132678182 1.25935462789e-005 0.000506941767553 0.115546239323 208.25211299 0.383355188918 0.00423671489079 0.00576328510921 0.00576328510921 309.668007088 1466560 0.0207632851092 586.674718834 1.25595733383e-005 0.000500686985432 0.110485882766 183.712193579 0.408912201513 0.00443188229163 0.00556811770837 0.00556811770837 309.161339656 1466560 0.0205681177084 588.15900417 1.25270590184e-005 0.000494729045075 0.105628324245 160.17117299 0.434469214107 0.00461846606509 0.00538153393491 0.00538153393491 308.681887831 1466560 0.0203815339349 589.589027188 1.24959206153e-005 0.000489052049408 0.100971685443 137.561661296 0.460026226702 0.00479682108591 0.00520317891409 0.00520317891409 308.214102806 1466560 0.0202031789141 590.996481298 1.24656236931e-005 0.000483617963397 0.0965227079919 115.284726017 0.485583239296 0.00496732010884 0.00503267989116 0.00503267989116 307.770531093 1466560 0.0200326798912 592.353671203 1.24365940749e-005 0.000478437900664 0.0922663882626 93.8643136369 0.511140251891 0.00513031865473 0.00486968134527 0.00486968134527 307.354081846 1466560 0.0198696813453 593.653096203 1.24089260809e-005 0.000473506313678 0.0881951779446 73.4411112278 0.536697264485 0.00528613644989 0.00471386355011 0.00471386355011 306.944458972 1466560 0.0197138635501 594.937510001 1.23819185676e-005 0.000468778844207 0.0843164979997 53.2112960427 0.56225427708 0.00543509041476 0.00456490958524 0.00456490958524 306.549596831 1466560 0.0195649095852 596.189068702 1.23558374806e-005 0.000464260190779 0.0806186061801 33.5117279836 0.587811289674 0.00557751252659 0.00442248747341 0.00442248747341 306.183234029 1466560 0.0194224874734 597.376899451 1.23311448569e-005 0.000459964204021 0.077086485886 14.9214237654 0.613368302269 0.00571370394431 0.00428629605569 0.00428629605569 305.833808367 1466560 0.0192862960557 598.525346283 1.23074353494e-005 0.000455862524989 0.0737206119724 -3.01587864549 0.638925314863 0.00584395466285 0.00415604533715 0.00415604533715 305.496591436 1466560 0.0191560453371 599.644174529 1.22845375013e-005 0.000451939027192 0.0705167923718 -20.4817806862 0.664482327458 0.00596856567408 0.00403143432592 0.00403143432592 305.177553599 1466560 0.0190314343259 600.719610467 1.22626445103e-005 0.000448195322769 0.0674645371299 -37.2178474339 0.690039340052 0.00608780167595 0.00391219832405 0.00391219832405 304.875074424 1466560 0.018912198324 601.754599704 1.22416908502e-005 0.000444621238417 0.0645582361014 -53.2786988301 0.715596352647 0.00620190716618 0.00379809283382 0.00379809283382 304.585851444 1466560 0.0187980928338 602.755956523 1.22215538225e-005 0.000441204454298 0.0617932530088 -68.7907545513 0.741153365242 0.00631113549352 0.00368886450648 0.00368886450648 304.310172934 1466560 0.0186888645065 603.7226108 1.22022319721e-005 0.000437938456191 0.0591627407475 -83.7329715482 0.766710377836 0.00641572521999 0.00358427478001 0.00358427478001 304.04848953 1466560 0.01858427478 604.653136049 1.21837296234e-005 0.000434817402763 0.0566600789412 -98.0779159765 0.792267390431 0.00651590751421 0.00348409248579 0.00348409248579 303.799403648 1466560 0.0184840924858 605.550347308 1.21659873389e-005 0.00043183265902 0.0542795435438 -111.876697678 0.817824403025 0.00661190602773 0.00338809397227 0.00338809397227 303.562986606 1466560 0.0183880939723 606.413792535 1.21489958035e-005 0.000428978230211 0.0520148795685 -125.119700767 0.84338141562 0.00670391955534 0.00329608044466 0.00329608044466 303.338622742 1466560 0.0182960804447 607.244575524 1.21327235632e-005 0.000426247678113 0.0498606778805 -137.826507724 0.868938428214 0.00679213640346 0.00320786359654 0.00320786359654 303.125059066 1466560 0.0182078635965 608.045314159 1.21171175106e-005 0.000423633849748 0.0478119585943 -150.044589562 0.894495440809 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0.000372996451021 0.0127872400224 -389.417470627 1.8656619194 0.00856210059916 0.00143789940084 0.00143789940084 299.437578954 1466560 0.0164378994008 624.536323801 1.18118234271e-005 0.000372354172549 0.0124341720389 -392.363495011 1.891218932 0.00858425997466 0.00141574002534 0.00141574002534 299.402258335 1466560 0.0164157400253 624.741505969 1.18082116186e-005 0.000371730088079 0.0120943826407 -395.220859333 1.91677594459 0.00860581386581 0.00139418613419 0.00139418613419 299.368228903 1466560 0.0163941861342 624.940934723 1.18047056199e-005 0.000371123536593 0.0117672894553 -397.993173615 1.94233295718 0.00862678850887 0.00137321149113 0.00137321149113 299.335459506 1466560 0.0163732114911 625.134774476 1.18013018326e-005 0.000370533793374 0.0114522529844 -400.682719068 1.96788996978 0.00864720672771 0.00135279327229 0.00135279327229 299.303914194 1466560 0.0163527932723 625.323187325 1.17979968401e-005 0.000369960214716 0.0111487032229 -403.291844303 1.99344698237 0.00866708543922 0.00133291456078 0.00133291456078 299.273539391 1466560 0.0163329145608 625.506351262 1.17947872468e-005 0.000369402283355 0.0108561745875 -405.823396497 2.01900399497 0.00868644284443 0.00131355715557 0.00131355715557 299.24430088 1466560 0.0163135571556 625.68440569 1.17916701594e-005 0.000368859477792 0.0105741926797 -408.27945656 2.04456100756 0.00870529715231 0.00129470284769 0.00129470284769 299.21615189 1466560 0.0162947028477 625.857524487 1.17886422369e-005 0.000368331257886 0.0103022964345 -410.662711034 2.07011802016 0.00872367327227 0.00127632672773 0.00127632672773 299.188937667 1466560 0.0162763267277 626.026192626 1.17856956963e-005 0.000367816751194 0.0100399496436 -412.981186147 2.09567503275 0.00874158374589 0.00125841625411 0.00125841625411 299.162667377 1466560 0.0162584162541 626.190418979 1.17828296935e-005 0.000367315647115 0.00978679352152 -415.234772882 2.12123204535 0.00875904434451 0.00124095565549 0.00124095565549 299.137291694 1466560 0.0162409556555 626.350379273 1.17800410178e-005 0.000366827465309 0.00954243731032 -417.426237037 2.14678905794 0.00877606987246 0.00122393012754 0.00122393012754 299.112762644 1466560 0.0162239301275 626.506242913 1.17773265973e-005 0.00036635175255 0.00930651371821 -419.558254716 2.17234607054 0.0087926773221 0.0012073226779 0.0012073226779 299.089087601 1466560 0.0162073226779 626.6580541 1.17746849954e-005 0.000365888080785 0.00907863074369 -421.631137857 2.19790308313 0.00880888075208 0.00119111924792 0.00119111924792 299.066241632 1466560 0.0161911192479 626.805924195 1.17721139825e-005 0.000365436050043 0.00885844951036 -423.646517696 2.22346009572 0.00882469242493 0.00117530757507 0.00117530757507 299.044186961 1466560 0.0161753075751 626.949988836 1.17696110778e-005 0.000364995287891 0.00864566509287 -425.606525433 2.24901710832 0.00884012461839 0.00115987538161 0.00115987538161 299.022903978 1466560 0.0161598753816 627.090339625 1.17671744087e-005 0.000364565448301 0.00843997876557 -427.512485505 2.27457412091 0.00885519015986 0.00114480984014 0.00114480984014 299.002351289 1466560 0.0161448098401 627.227127966 1.17648012879e-005 0.000364146139084 0.0082410936158 -429.366769956 2.30013113351 0.00886990489601 0.00113009510399 0.00113009510399 298.982419234 1466560 0.016130095104 627.360696952 1.17624863523e-005 0.000363736789942 0.00804868525236 -431.175077682 2.3256881461 0.00888427778111 0.00111572221889 0.00111572221889 298.96311647 1466560 0.0161157222189 627.491053176 1.17602290341e-005 0.000363337182516 0.00786251981807 -432.937302697 2.3512451587 0.00889831957565 0.00110168042435 0.00110168042435 298.944406223 1466560 0.0161016804244 627.618329704 1.17580270059e-005 0.000362946985099 0.00768234877234 -434.655540832 2.37680217129 0.0089120404309 0.0010879595691 0.0010879595691 298.926251754 1466560 0.0160879595691 627.742657429 1.17558780018e-005 0.000362565881848 0.00750793756747 -436.331865613 2.40235918389 0.0089254518473 0.0010745481527 0.0010745481527 298.908702318 1466560 0.0160745481527 627.863958036 1.17537825329e-005 0.000362193648041 0.00733903537029 -437.964510036 2.42791619648 0.00893856299001 0.00106143700999 0.00106143700999 298.891731443 1466560 0.01606143701 627.98233294 1.17517387786e-005 0.000361830008249 0.00717543172666 -439.55504169 2.45347320908 0.00895138252366 0.00104861747634 0.00104861747634 298.875317464 1466560 0.0160486174763 628.097869589 1.17497451322e-005 0.000361474707046 0.00701692728302 -441.104790086 2.47903022167 0.00896391887358 0.00103608112642 0.00103608112642 298.859454989 1466560 0.0160360811264 628.210613688 1.17478005629e-005 0.000361127519006 0.00686332959232 -442.614335219 2.50458723426 0.0089761814047 0.0010238185953 0.0010238185953 298.844099681 1466560 0.0160238185953 628.320716369 1.17459026004e-005 0.000360788137492 0.00671444165955 -444.086114067 2.53014424686 0.00898818087484 0.00101181912516 0.00101181912516 298.829155164 1466560 0.0160118191252 628.428470485 1.17440468362e-005 0.000360456143966 0.00657005737715 -445.525055336 2.55570125945 0.00899992365436 0.00100007634564 0.00100007634564 298.814639981 1466560 0.0160000763456 628.53385208 1.17422332703e-005 0.000360131401249 0.00643002218795 -446.930549435 N $not all material ports are connectedethane productionLengthLengthReactor lengthParameter Length3Virtual information port linked to parameter Length?Lengthj@InletParameter LengthOutlet  @@ @@ @@ @@ @@ ??@@@@Measure1TMeasureUnit - unit operation to expose material stream values as information streamsV KIeQ%COUSCOUS0002Thermo Version*Thermodynamics CAPE-OPEN Interface version1.01.01.01.1Normal pressure-Pressure for calculation of normal properties?м@м@ _BNormal temperature0Temperature for calculation of normal properties?fffffr@fffffr@ _BEthyleneComponent mole flow(Ethylene)O $not all material ports are connectedInletOutletComponent mole 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